CN101530720A - Acid fog absorption tower - Google Patents
Acid fog absorption tower Download PDFInfo
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- CN101530720A CN101530720A CN200910025986A CN200910025986A CN101530720A CN 101530720 A CN101530720 A CN 101530720A CN 200910025986 A CN200910025986 A CN 200910025986A CN 200910025986 A CN200910025986 A CN 200910025986A CN 101530720 A CN101530720 A CN 101530720A
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Abstract
The invention discloses an acid fog absorption tower, which comprises a cylindrical tower body, wherein the upper end of the tower body is connected with an exhaust pipe, the lower part of the tower body is connected with a water tank, the side wall of the tower body is connected with an air intake, the inside of the tower body is provided with a vapor-water separator, a packing layer, a guide barrel and a three-stage spray pipe form top to bottom; the water tank is communicated with the three-stage spray pipe through a connecting pipe and a circulating water pump, and the three-stage spray pipe consists of an upper spray pipe, an intermediate spray pipe, and a lower spray pipe; the upper spray pipe and the lower spray pipe are communicated with a water distributor respectively; the water distributor comprises a main water inlet pipe and a branch water distribution pipe communicated with the main water inlet pipe, and the branch water distribution pipe is provided with a helical spray head; and the guide barrel is positioned between the upper spray pipe and the intermediate spray pipe, a defrosting pan is fixedly connected between the guide barrel and the tower body, and the upper part of the guide barrel is provided with a water retaining ring plate. The absorption tower has removal rate up to 100 percent, and has the advantages of small resistance, small energy consumption, high treatment efficiency, compact structure, corrosion resistance, aging resistance, and the like.
Description
Technical field
The present invention relates to a kind for the treatment of apparatus of industrial waste acid water, particularly a kind of acid fog absorption tower with the acid mist absorption function of making laughs.
Background technology
In the industrial production factory, produce a large amount of acid waste liquids through regular meeting.Acid waste liquid all has very big harm to the equipment of industrial product and environment, and, along with China is more and more higher to the requirement that industry energy conservation reduces discharging, acid waste liquid is removed become to attach most importance to problem.Traditional spray column uses simple neutralisation treatment mode, therefore handles effective clearance of acid mist generally about 85%.The tradition absorption tower is a primary and secondary perforation tubular type water distribution, has the water distribution inequality, and air-flow liquid contacts inadequate shortcoming.And water distribution manner is simple, and the reaction time does not often reach designing requirement.
Summary of the invention
Goal of the invention: technical problem to be solved by this invention is at the deficiencies in the prior art, and a kind of acid fog absorption tower is provided.
Technical scheme: the invention discloses a kind of acid fog absorption tower, comprise cylindrical tower body, the tower body upper end is connected with blast pipe, and the tower body bottom is connected with water tank, the tower body sidewall is connected with air inlet, is provided with steam-water separator, packing layer, guide shell and three grades of showers from top to bottom in tower body inside; Described water tank is communicated with described three grades of showers by tube connector and water circulating pump, and described three grades of showers are made of upper spray pipe, middle shower, lower spray pipe; Described upper spray pipe and lower spray pipe are communicated with water-locator respectively; Described water-locator comprises the water distribution branch pipe that water into is responsible for and is communicated with it, is provided with spiral spray head on water distribution branch pipe; Described guide shell is fixedly connected with drip tray between guide shell and tower body between upper spray pipe and middle shower, be provided with the dash girth sheets on guide shell top.
Among the present invention, preferably, described spiral spray head is provided with the spray nozzle of conical hollow rotary drilling-head shape.
Among the present invention, preferably, described steam-water separator is several S shape steel plates that is parallel to each other and connects.
Among the present invention, preferably, described water distribution branch pipe is connected with tower body by supporting supporting plate, thereby can strengthen the stability of water-locator.
Among the present invention, preferably, described water tank is provided with visor, is convenient to observe buck water level in the water tank thus, adds water in real time.
Among the present invention, preferably, the described guide shell first half is turned letter heart truncated cone-shaped, and Lower Half is a hollow cylinder.The buck of shower was through the guide shell diffusion in the middle of this design can guarantee.
Among the present invention, preferably, described drip tray open circles plate-like, disk body is provided with the venetian blind type disc space and with angle along radial direction.
The present invention, in, preferably, described dash girth sheets is fixedlyed connected with the stiffener that is arranged on the tower body inwall.
Beneficial effect: the guide shell design of creating in the acid fog absorption tower of the present invention, be equipped with the drip tray of the shutter form of certain angle setting, make the spray liquid and the pernicious gas of rising be blended in rotation at a high speed in the tower, strengthen gas-liquid contact area and time, improved the removal efficient of pernicious gas greatly, effective clearance on domestic traditional absorption tower is generally about 85%, and the clearance on this novel absorption tower can reach 100%.
Tower body is composite glass fiber reinforced acid fog absorption tower among the present invention, also can be carbon steel or stainless steel, this equipment has that resistance is little, the saving energy, noise is low, treatment effeciency is high, compact conformation, floor space is little, corrosion-resistant, ageing-resistant performance is good, in light weight, be convenient to characteristics such as installation, transportation, management, maintenance, is the desirable cleaning equipment of desirable waste gas such as processing alkali steam, ammonia, hydrogen chloride, hydrogen fluoride, sulfuric acid mist, alcohol, citric acid, hydrogen sulfide and nitrogen oxide.
Description of drawings
Below in conjunction with the drawings and specific embodiments the present invention is done further to specify, above-mentioned and/or otherwise advantage of the present invention will become apparent.
Fig. 1 is a structural representation of the present invention.
Fig. 2 is water-locator part schematic diagram among the present invention.
Fig. 3 is spiral spray head schematic diagram among the present invention.
Fig. 4 is a spray nozzle partial enlarged drawing on the spiral spray head.
Fig. 5 is guide shell part schematic diagram in the tower body among the present invention.
Fig. 6 is drip tray schematic diagram among the present invention.
The specific embodiment:
As shown in Figure 1, the invention discloses a kind of acid fog absorption tower, comprise cylindrical tower body 1, the tower body upper end is connected with blast pipe 2, the tower body bottom is connected with water tank 3, the tower body sidewall is connected with air inlet 4, is provided with steam-water separator 5, packing layer 6, guide shell 7 and three grades of showers from top to bottom in tower body inside; Described water tank 3 is communicated with described three grades of showers by tube connector and water circulating pump 8, and described three grades of showers are made of upper spray pipe 9, middle shower 10, lower spray pipe 11; Described upper spray pipe 9 and lower spray pipe 11 are communicated with water-locator 12 respectively.As shown in Figure 2, described water-locator 12 comprises that water into is responsible for 13 and the water distribution branch pipe 14 that is communicated with it.As shown in Figure 3 and Figure 4, be provided with spiral spray head 15 on water distribution branch pipe 14, spiral spray head 15 is provided with the spray nozzle 21 of conical hollow rotary drilling-head shape.Described steam-water separator 5 is several S shape steel plates that is parallel to each other and connects.Described water distribution branch pipe 14 is connected with tower body 1 by supporting supporting plate 16.Described water tank 3 is provided with visor 17.Also be provided with upper valve 18, middle valve 19 and bottom valve 20 on described upper spray pipe 9, middle shower 10, the lower spray pipe 11.
As shown in Figure 5, be fixedly connected with drip tray 22 between guide shell 7 and tower body 1, be provided with dash girth sheets 23 on guide shell 7 tops, described guide shell 7 first halves are turned letter heart truncated cone-shaped, and Lower Half is a hollow cylinder.As shown in Figure 6, described drip tray 22 open circles plate-likes, disk body is provided with venetian blind type disc 24 space and with angle along radial direction.Described dash girth sheets 23 is fixedlyed connected with the stiffener 25 that is arranged on the tower body inwall.
This tower is that employing 2-6% sodium hydroxide solution is a neutralizer, handling sulfuric acid mist simultaneously, the gas that citric acid, alcohol produced also is purified simultaneously, and also replaceable neutralizer is used to handle waste gas such as alkali steam, ammonia, hydrogen fluoride, hydrogen sulfide and nitrogen oxide.
The tradition absorption tower is a primary and secondary perforation tubular type water distribution, has the water distribution inequality, and air-flow liquid contacts inadequate shortcoming.As shown in Figure 3 and Figure 4, the spray nozzle 21 of the conical hollow rotary drilling-head shape of creating among the present invention, spray nozzle 21 delivery port pressure are greater than 0.3Kgf/cm
2, the jet flow angular range can be 60 °～170 °.3 the crust pressure under, the liquid flow rate scope be the 5.5-4140 liter/minute.Each spray nozzle pressure is even, helps the uniformity of water distribution, and spray liquid is descended with vaporific sprinkling, and the gas-liquid full contact is eliminated the water distribution dead angle, avoids the water distribution uneven phenomenon.The shower nozzle of this compact conformation has unimpeded runner design, can farthest reduce liquid lock, makes liquid reach maximum stream flow on the pipeline of intended size.The operation principle of spiral spray head is: liquid (or slip) by and collision tangent with the helicoid that diminishes continuously after, become the ejection of small liquid pearl and form vaporific.It is minimum that airflow design from import to outlet in the shower nozzle cavity makes resistance coefficient reduce to, thereby spiral nozzle is applicable to numerous industrial circles such as chemical industry, environmental protection, electric power, weaving, and particularly the flue gas desulfurization and dedusting sector application is more extensive.
The invention provides a kind of thinking and method of acid fog absorption tower; the method and the approach of this technical scheme of specific implementation are a lot; the above only is a preferred implementation of the present invention; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the principle of the invention, can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.The all available prior art of each component part not clear and definite in the present embodiment is realized.
Claims (8)
1, a kind of acid fog absorption tower, it is characterized in that, comprise cylindrical tower body (1), the tower body upper end is connected with blast pipe (2), the tower body bottom is connected with water tank (3), the tower body sidewall is connected with air inlet (4), is provided with steam-water separator (5), packing layer (6), guide shell (7) and three grades of showers from top to bottom in tower body inside; Described water tank (3) is communicated with described three grades of showers by tube connector and water circulating pump (8), and described three grades of showers are made of upper spray pipe (9), middle shower (10), lower spray pipe (11); Described upper spray pipe (9) and lower spray pipe (11) are communicated with water-locator (12) respectively; Described water-locator (12) comprises the water distribution branch pipe (14) that water into is responsible for (13) and is communicated with it, is provided with spiral spray head (15) on water distribution branch pipe (14); Described guide shell (7) is positioned between upper spray pipe (9) and the middle shower (10), is fixedly connected with drip tray (22) between guide shell (7) and tower body (1), is provided with dash girth sheets (23) on guide shell (7) top.
2, acid fog absorption tower according to claim 1 is characterized in that, described spiral spray head (15) is provided with the spray nozzle (21) of conical hollow rotary drilling-head shape.
3, acid fog absorption tower according to claim 1 and 2 is characterized in that, described steam-water separator (5) is several S shape steel plates that is parallel to each other and connects.
4, acid fog absorption tower according to claim 3 is characterized in that, described water distribution branch pipe (14) is connected with tower body (1) by supporting supporting plate (16).
5, acid fog absorption tower according to claim 4 is characterized in that, described water tank (3) is provided with visor (17).
6, acid fog absorption tower according to claim 1 is characterized in that, described guide shell (7) first half is turned letter heart truncated cone-shaped, and Lower Half is a hollow cylinder.
7, acid fog absorption tower according to claim 6 is characterized in that, described drip tray (22) open circles plate-like, and disk body is provided with venetian blind type disc (24) space and with angle along radial direction.
8, acid fog absorption tower according to claim 7 is characterized in that, described dash girth sheets (23) is fixedlyed connected with the stiffener that is arranged on the tower body inwall (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100259867A CN101530720B (en) | 2009-03-16 | 2009-03-16 | Acid fog absorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100259867A CN101530720B (en) | 2009-03-16 | 2009-03-16 | Acid fog absorption tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101530720A true CN101530720A (en) | 2009-09-16 |
| CN101530720B CN101530720B (en) | 2011-01-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009100259867A Expired - Fee Related CN101530720B (en) | 2009-03-16 | 2009-03-16 | Acid fog absorption tower |
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| CN (1) | CN101530720B (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101972575A (en) * | 2010-07-28 | 2011-02-16 | 苏州顶裕节能设备有限公司 | Guide waterproof device of washing tower inlet |
| CN101732951B (en) * | 2009-12-25 | 2013-04-10 | 青岛科技大学 | Organic waste gas treatment equipment |
| CN103263817A (en) * | 2013-06-03 | 2013-08-28 | 胡乃正 | Gas purification device |
| CN104676619A (en) * | 2015-01-28 | 2015-06-03 | 燕山大学 | Device combining fuel gas boiler chimney and spraying type smoke waste heat recycling component |
| CN104941391A (en) * | 2014-12-23 | 2015-09-30 | 江苏大峘集团有限公司 | Device for removing hydrogen chloride gas in flue gas |
| CN105435592A (en) * | 2015-12-07 | 2016-03-30 | 东营科创生物化工有限公司 | Drying bed ammonia absorption tower |
| CN105498410A (en) * | 2016-02-04 | 2016-04-20 | 杨青淼 | Flexible pull-type washing tower |
| CN105597496A (en) * | 2015-12-31 | 2016-05-25 | 浙江平湖华龙实业股份有限公司 | Sulfuric acid mist purification device of high-performance storage battery |
| CN105669427A (en) * | 2016-02-26 | 2016-06-15 | 程洪光 | Recover method for acid mist generated by acid hydrolysis reaction in citric acid production |
| CN107462085A (en) * | 2017-09-22 | 2017-12-12 | 北京华誉能源技术股份有限公司 | A kind of flue gas waste heat recovery system and method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2751869Y (en) * | 2004-11-26 | 2006-01-18 | 北京西山除尘器厂 | Dust removal peculiar smell removing multifunction purifying tower |
| CN2845894Y (en) * | 2005-11-28 | 2006-12-13 | 宜兴市意德环保水处理设备有限公司 | Acid mist absorptive purifying tower |
| CN101279196A (en) * | 2008-05-27 | 2008-10-08 | 湖北三新磷钙有限公司 | Double return route absorption tower and method for treating fluorine contained tail gas using double return route absorption tower |
-
2009
- 2009-03-16 CN CN2009100259867A patent/CN101530720B/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101732951B (en) * | 2009-12-25 | 2013-04-10 | 青岛科技大学 | Organic waste gas treatment equipment |
| CN101972575A (en) * | 2010-07-28 | 2011-02-16 | 苏州顶裕节能设备有限公司 | Guide waterproof device of washing tower inlet |
| CN103263817A (en) * | 2013-06-03 | 2013-08-28 | 胡乃正 | Gas purification device |
| CN104941391B (en) * | 2014-12-23 | 2017-08-29 | 大峘集团有限公司 | A kind of flue gas removes the device of hydrogen chloride gas |
| CN104941391A (en) * | 2014-12-23 | 2015-09-30 | 江苏大峘集团有限公司 | Device for removing hydrogen chloride gas in flue gas |
| CN104676619A (en) * | 2015-01-28 | 2015-06-03 | 燕山大学 | Device combining fuel gas boiler chimney and spraying type smoke waste heat recycling component |
| CN105435592A (en) * | 2015-12-07 | 2016-03-30 | 东营科创生物化工有限公司 | Drying bed ammonia absorption tower |
| CN105597496A (en) * | 2015-12-31 | 2016-05-25 | 浙江平湖华龙实业股份有限公司 | Sulfuric acid mist purification device of high-performance storage battery |
| CN105498410A (en) * | 2016-02-04 | 2016-04-20 | 杨青淼 | Flexible pull-type washing tower |
| CN105498410B (en) * | 2016-02-04 | 2017-06-30 | 宁波飞源环保工程科技有限公司 | Flexible pull-type scrubbing tower |
| CN105669427A (en) * | 2016-02-26 | 2016-06-15 | 程洪光 | Recover method for acid mist generated by acid hydrolysis reaction in citric acid production |
| CN107462085A (en) * | 2017-09-22 | 2017-12-12 | 北京华誉能源技术股份有限公司 | A kind of flue gas waste heat recovery system and method |
| CN107462085B (en) * | 2017-09-22 | 2023-12-26 | 北京华誉能源技术股份有限公司 | Flue gas waste heat recovery system and method |
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| Publication number | Publication date |
|---|---|
| CN101530720B (en) | 2011-01-05 |
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| C56 | Change in the name or address of the patentee |
Owner name: JIANGSU ZHANHONG ENVIRONMENTAL PROTECTION TECHNOLO Free format text: FORMER NAME: JIANGSU ZHANHONG ENVIRONMENT PROTECTION EQUIPMENT CO., LTD. |
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| CP01 | Change in the name or title of a patent holder |
Address after: 214214 Jiangsu city of Yixing province Gaocheng town northeast of Xincheng Road No. 29 Patentee after: Jiangsu grand Environmental Protection Technology Co., Ltd. Address before: 214214 Jiangsu city of Yixing province Gaocheng town northeast of Xincheng Road No. 29 Patentee before: Jiangsu Zhanhong Environment Protection Equipment Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110105 Termination date: 20150316 |
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| EXPY | Termination of patent right or utility model |